CN1224449C - Membrane filtration manifold system - Google Patents
Membrane filtration manifold system Download PDFInfo
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- CN1224449C CN1224449C CNB008064695A CN00806469A CN1224449C CN 1224449 C CN1224449 C CN 1224449C CN B008064695 A CNB008064695 A CN B008064695A CN 00806469 A CN00806469 A CN 00806469A CN 1224449 C CN1224449 C CN 1224449C
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D63/00—Apparatus in general for separation processes using semi-permeable membranes
- B01D63/02—Hollow fibre modules
- B01D63/04—Hollow fibre modules comprising multiple hollow fibre assemblies
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D65/00—Accessories or auxiliary operations, in general, for separation processes or apparatus using semi-permeable membranes
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D63/00—Apparatus in general for separation processes using semi-permeable membranes
- B01D63/02—Hollow fibre modules
- B01D63/031—Two or more types of hollow fibres within one bundle or within one potting or tube-sheet
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D63/00—Apparatus in general for separation processes using semi-permeable membranes
- B01D63/02—Hollow fibre modules
- B01D63/04—Hollow fibre modules comprising multiple hollow fibre assemblies
- B01D63/046—Hollow fibre modules comprising multiple hollow fibre assemblies in separate housings
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2313/00—Details relating to membrane modules or apparatus
- B01D2313/06—External membrane module supporting or fixing means
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2313/00—Details relating to membrane modules or apparatus
- B01D2313/12—Specific discharge elements
- B01D2313/125—Discharge manifolds
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2313/00—Details relating to membrane modules or apparatus
- B01D2313/21—Specific headers, end caps
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2315/00—Details relating to the membrane module operation
- B01D2315/06—Submerged-type; Immersion type
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Abstract
Description
发明领域field of invention
本发明涉及一种薄膜过滤管系统。更确切地,本发明涉及一种用于中空纤维薄膜过滤器的薄膜过滤管系统,该系统包括细长的中空纤维薄膜束,其中需要过滤的物料是通过运送到纤维束外部而进行过滤的,而滤出液是从纤维内腔的一端或若干端进行排出的。上述系统同样最好包括用于对纤维供料表面进行定期性清洗的清洗装置。The invention relates to a membrane filter tube system. More precisely, the present invention relates to a membrane filter tube system for a hollow fiber membrane filter, the system comprising bundles of elongated hollow fiber membranes, wherein the material to be filtered is filtered by being conveyed outside the bundle, The filtrate is discharged from one or several ends of the fiber lumen. The above system also preferably includes cleaning means for periodically cleaning the fiber supply surface.
本发明一直主要应用在对大气压力开放的薄膜过滤系统中,以下将对此进行描述。然而,应当理解到本发明并不限于上述特定的使用领域。The invention has been primarily used in membrane filtration systems open to atmospheric pressure, as will be described below. It should be understood, however, that the present invention is not limited to the specific fields of use described above.
现有技术的描述Description of prior art
现有技术中通常的过滤管是应用在上述过滤系统中。这些过滤系统通常包括细长管状滤芯,其包围着一束中空纤维薄膜。管或集管的布置用于连接上述芯,通常在一端或两端进行连接,这些管用来使污染的物料、滤出液以及清洗液的各个流动通过该系统发生分离和转向。在此,横流系统通常具有两个物料管(进口和再循环出口)以及一个或两个过滤管。在现有技术的横流过滤系统中,需要被过滤的物料流与薄膜表面相切或穿过薄膜表面而流动。这就对薄膜表面产生了一个清扫作用,使其更清洁。相反,设置为闭端操作的系统在过滤模式中仅能利用一个物料入口管和一个过滤出口管。另外,这些现有技术中管或集管的布置常常设置成为方便构造成模块化的两维或三维芯阵列。Common filter tubes in the prior art are used in the above filter system. These filtration systems typically consist of an elongated tubular filter element surrounding a bundle of hollow fiber membranes. An arrangement of tubes or headers is used to connect the cores, usually at one or both ends, and these tubes are used to separate and divert the individual flows of contaminated material, filtrate and cleaning fluid through the system. Here, cross-flow systems generally have two material pipes (inlet and recirculation outlet) and one or two filter pipes. In prior art cross-flow filtration systems, the stream of material to be filtered flows tangentially to or across the membrane surface. This creates a sweeping action on the surface of the film, making it cleaner. In contrast, a system set up for closed-end operation can only utilize one material inlet tube and one filter outlet tube in filter mode. Additionally, these prior art arrangements of tubes or headers are often arranged in such a way that they are conveniently constructed as modular two- or three-dimensional arrays of cores.
更典型地,现有技术中的过滤系统如上所述,相对大气是密闭的。在该系统中,需要过滤的流体(以下称之为物料)是在正压力下被输送到过滤器的。为了使这种类型的系统有效操作,上述细长的管状过滤筒被装入气密外壳中。这种外壳随后再与既分离物料和滤出液又支承该气密外壳的过滤管管系统相连。这种过滤管系统也可以用于将清洗液引入过滤系统。More typically, prior art filtration systems, as described above, are closed to the atmosphere. In this system, the fluid to be filtered (hereinafter referred to as material) is conveyed to the filter under positive pressure. In order for this type of system to operate efficiently, the aforementioned elongated tubular filter cartridge is encased in an airtight enclosure. This housing is then connected to a filter tube system which both separates the material and filtrate and supports the airtight housing. This filter tube system can also be used to introduce cleaning fluid into the filter system.
现有技术中的过滤系统,如上所述,也可以对大气环境开放。在该系统中很典型的是,物料是在负压力下穿过薄膜进行提取的。这是通过在薄膜的滤出液侧施加一个负压力或吸力而实现的。这种系统相比与大气相密闭的系统而言易于应用更少的基础设施和基本工作,这是因为它们不再需要要求具有相对较高压力的元件。例如,在对大气开放的系统中,无需将过滤筒装入单个气密外壳中。在这些系统中很典型的是,过滤筒仅仅是基本浸入一个装有物料的开口箱中。在这个系统中,希望设置一个合适的管,用来支承过滤筒并使滤出液在分离出物料和滤出液的同时从过滤器中抽取出。相似地,与密闭系统一样,这种过滤管也可以用于支承一个清洗液系统的目的。Filtration systems in the prior art, as described above, may also be open to the atmosphere. Typically in this system, material is extracted through a membrane under negative pressure. This is accomplished by applying a negative pressure or suction on the filtrate side of the membrane. Such systems tend to employ less infrastructure and capital work than systems closed to the atmosphere, since they no longer require components requiring relatively high pressures. For example, in a system that is open to the atmosphere, it is not necessary to house filter cartridges into a single airtight housing. Typically in these systems, the filter cartridge is only substantially submerged in an open box containing the material. In this system, it is desirable to provide a suitable tube for supporting the filter cartridge and allowing filtrate to be drawn from the filter while the material and filtrate are being separated. Similarly, as with closed systems, such filter tubes may also serve the purpose of supporting a cleaning fluid system.
现有技术的过滤系统及其相关的上述过滤筒通常具有复杂的管道和部件布置,组装起来很困难并且费时。另外,现有技术的过滤系统中实际的过滤管系统元件自身也常常是一个复杂的部件组合。Prior art filtration systems and their associated aforementioned filter cartridges typically have complex piping and component arrangements that are difficult and time consuming to assemble. Additionally, the actual filter tube system components in prior art filtration systems are often a complex assembly of components themselves.
上述现有技术的过滤系统也需要常规检测来评定系统的完整性。不完整可能是由于单个过滤薄膜中空纤维、O型圈或其它系统元件的故障。完整性检测通常需要拆卸任一单个系统元件或者过滤筒。在现有技术的传统过滤管中通常很难进行上述的拆卸操作。另外,如上所述,现有技术的过滤管可能包括许多复杂的部件。它随之要进行的对这些部件的完整性检测同样很费时。The prior art filtration systems described above also require routine testing to assess the integrity of the system. Incompleteness may be due to failure of individual filter membrane hollow fibers, O-rings, or other system components. Integrity testing typically requires disassembly of any individual system component or filter cartridge. The above-mentioned disassembly operation is generally difficult to perform in conventional filter tubes of the prior art. Additionally, as noted above, prior art filter tubes may include many complex components. The subsequent integrity checks of these components are likewise time-consuming.
本发明的目的是提供一种在此所述的过滤管系统,该系统至少能克服或改善现有技术中存在的一些缺陷,或者至少能提供一种有用的替代物。It is an object of the present invention to provide a filter tube system as described herein which overcomes or ameliorates at least some of the disadvantages of the prior art, or at least provides a useful alternative.
发明概述Summary of the invention
根据本发明的一个方面,提供了一个薄膜过滤管,用于连接一种具有一个或多个细长半透性聚合纤维束的过滤子模块,上述管包括:According to one aspect of the present invention there is provided a membrane filter tube for connection to a filter submodule having one or more elongated semipermeable polymeric fiber bundles, said tube comprising:
一个外壳,和a shell, and
至少一个与上述外壳相连的子模块连接轴环,该轴环适于接纳和定位上述子模块,上述子模块设有一个具有锁定结构的连接套管,由此该子模块能在一端被一个夹持装置固定在轴环上,上述夹持装置适于使上述轴环和上述锁定结构接合以便防止子模块沿轴向从轴环中脱出。At least one sub-module connection collar connected to the housing, the collar is suitable for receiving and positioning the above-mentioned sub-module, the above-mentioned sub-module is provided with a connection sleeve with a locking structure, whereby the sub-module can be clamped at one end by a The holding device is fixed on the collar, and the holding device is adapted to engage the collar with the locking structure so as to prevent the sub-module from coming out of the collar in the axial direction.
上述锁定结构最好包括一个形成在上述套管上的圆周凸缘。Preferably said locking structure comprises a peripheral flange formed on said sleeve.
同样,在一个最佳结构中,上述管的外壳和轴环在其之间还包括用于流体流通的通道。另外,上述外壳最好包括一个可拆卸的罩帽,用于与上述外壳形成气密性的密封接合。Also, in a preferred construction, the outer casing and collar of the tube further include a passage therebetween for fluid communication. Additionally, said housing preferably includes a removable cap for forming an airtight seal with said housing.
根据本发明的第二方面,提供了一个薄膜过滤装置,包括:According to a second aspect of the present invention, a membrane filtration device is provided, comprising:
一种具有一个或多个细长半透性聚合纤维束的过滤子模块;a filtration submodule having one or more bundles of elongated semipermeable polymeric fibers;
一个可拆卸地连接在上述过滤子模块一端的顶部元件;和a top element removably attached to one end of said filter submodule; and
一个可拆卸地连接在上述过滤子模块另一端的基部元件;a base element removably attached to the other end of said filter submodule;
上述顶部元件是根据本发明第一方面的薄膜过滤管。The above-mentioned top element is a membrane filter tube according to the first aspect of the present invention.
根据本发明的第三方面,提供了一个薄膜过滤装置排,包括:According to a third aspect of the present invention, there is provided a membrane filter arrangement comprising:
若干根据本发明第二方面的薄膜过滤装置;a number of membrane filtration devices according to the second aspect of the invention;
一个连接在至少一个薄膜过滤装置上的滤出液管道;和a filtrate conduit connected to at least one membrane filtration device; and
一个连接在至少一个薄膜过滤装置上的清洗液管道。A cleaning fluid line connected to at least one membrane filter unit.
上述模块组最好布置在一个垂直位置上,上述滤出液管道基本在上述顶部元件上方,上述清洗液管道基本在上述基部元件的上方。Said module set is preferably arranged in a vertical position, said filtrate conduit substantially above said top element and said cleaning fluid conduit substantially above said base element.
根据本发明的第四方面,提供了一个薄膜过滤装置阵列,包括若干通过一系列滤出液管道相连的根据本发明第三方面的薄膜过滤装置排。According to a fourth aspect of the present invention there is provided an array of membrane filtration devices comprising a number of rows of membrane filtration devices according to the third aspect of the invention connected by a series of filtrate conduits.
根据本发明的另一方面,提供了一个薄膜过滤装置阵列队,包括:According to another aspect of the present invention, an array of membrane filtration devices is provided, comprising:
一管道阵列队;和a pipeline array; and
若干通过上述管道阵列队相连的根据本发明第四方面的薄膜过滤装置阵列。Several membrane filtration device arrays according to the fourth aspect of the present invention are connected by the above pipeline array team.
附图的简要说明Brief description of the drawings
以下将仅以实例并结合附图描述本发明的最佳实施例:The preferred embodiment of the present invention will be described below only with examples and in conjunction with the accompanying drawings:
图1为本发明薄膜过滤管的透视图;Fig. 1 is the perspective view of membrane filter tube of the present invention;
图2为图1中薄膜过滤管的另一透视图;Fig. 2 is another perspective view of the membrane filter tube in Fig. 1;
图3为通过锁定夹持装置而与管轴环相连接的子模块的截面图;Figure 3 is a cross-sectional view of a submodule connected to a pipe collar by means of a locking clamp;
图4a为夹持装置的最佳实施例的等角图;Figure 4a is an isometric view of a preferred embodiment of the holding device;
图4b为图4a中最佳实施例夹持装置的等角图;Figure 4b is an isometric view of the preferred embodiment clamping device in Figure 4a;
图4c为夹持装置的替代实施例的等角图;Figure 4c is an isometric view of an alternative embodiment of a clamping device;
图5为图4a中锁定夹持装置的横截面侧视图;Figure 5 is a cross-sectional side view of the locking and clamping device of Figure 4a;
图6a示出上述轴环的一个细节;Figure 6a shows a detail of the aforementioned collar;
图6b示出上述轴环的另一个细节;Figure 6b shows another detail of the aforementioned collar;
图7a为过滤子模块中连接套管的一个实施例的俯视图;Figure 7a is a top view of an embodiment of the connecting sleeve in the filter sub-module;
图7b为沿图7a中A-A线所截取的图8a中连接套管的一个截面图;Fig. 7b is a cross-sectional view of the connecting sleeve in Fig. 8a taken along line A-A in Fig. 7a;
图7c为图7a中连接套管的一个侧剖视图;Fig. 7c is a side sectional view of the connecting sleeve in Fig. 7a;
图8a为过滤子模块中连接套管的替代实施例的俯视图;Figure 8a is a top view of an alternative embodiment of a connecting sleeve in a filter submodule;
图8b为沿图8a中B-B线所截取的图8a中连接套管的一个截面图;Fig. 8b is a sectional view of the connecting sleeve in Fig. 8a taken along the line B-B in Fig. 8a;
图8c为图8a中连接套管的一个侧视图;Figure 8c is a side view of the connecting sleeve in Figure 8a;
图9a为罩帽的一个透视图;Figure 9a is a perspective view of the cap;
图9b为图9a中罩帽的另一个透视图;Figure 9b is another perspective view of the cap in Figure 9a;
图10为图1中薄膜过滤管的一个透视图,其中示出图9中正在使用着的罩帽;Figure 10 is a perspective view of the membrane filter tube in Figure 1, showing the cover cap in use in Figure 9;
图11为薄膜过滤装置排的一个侧视图;Figure 11 is a side view of the row of membrane filtration devices;
图12a为薄膜过滤管在基部构造的一个侧面横截面图,其中示出清洗液从清洗液管道流经基部;Figure 12a is a side cross-sectional view of a membrane filter tube constructed at the base, showing cleaning fluid flowing through the base from the cleaning fluid piping;
图12b为薄膜过滤管在基部构造的一个正面横截面图,其中示出清洗液从清洗液管道流经基部;Figure 12b is a frontal cross-sectional view of a membrane filter tube constructed at the base, showing cleaning fluid flowing through the base from the cleaning fluid pipeline;
图13为薄膜过滤装置阵列的一个俯视图;Figure 13 is a top view of the array of membrane filtration devices;
图14为在薄膜过滤装置阵列中的一个薄膜过滤装置排的透视图;Figure 14 is a perspective view of a membrane filter row in a membrane filter array;
图15为薄膜过滤装置阵列队的一个等角图。Figure 15 is an isometric view of an array of membrane filtration devices.
最佳实施例的描述Description of the preferred embodiment
现在描述视图,薄膜过滤管系统包括一个薄膜过滤管1,用于连接一种包括细长中空纤维薄膜束的过滤子模块2。图1和图2很好地示出,管的最佳实施例包括一个与四个子模块连接轴环4相连的外壳3。Referring now to the views, the membrane filter tube system comprises a membrane filter tube 1 for connection to a
如图3所示,该轴环4适于接纳和定位上述子模块2,上述子模块2设有一个具有锁定凸缘6的连接套管5。在该实施例中,子模块2能在一端被一个夹持装置7固定在相应的轴环4上,上述夹持装置7同时使上述子模块2和锁定凸缘6接合在一起,以便防止子模块2沿轴向从轴环4中脱出。锁定凸缘6进一步与轴环4的唇部8形成支承接合。接合和释放夹持装置7基本上能使子模块2与管1容易地进行相应的组合和拆卸。管1另外还包括一个位于上述外壳3和轴环4之间的用于流体流通的滤出液通道9和一个用于与清洗液管道11实现清洗液流通的清洗液通道10。As shown in FIG. 3 , this
图4a、4b和5示出夹持装置7的最佳实施例。该夹持装置7具有一个基本为圆柱形的侧壁12,该侧壁12具有顶部凸缘13和底部凸缘14,每个凸缘都从侧壁12沿径向向内突出。该夹持装置7沿着一条平行与子模块2的直线被分割,以便允许夹持装置在沿轴向滑进或滑出与轴环4的锁定接合时能径向扩展。径向扩展是通过手动分开一对分别设在夹持装置凸缘13上并在裂口两侧上的突出物40而实现的。另外,夹持装置7弹性偏置以便能使夹持装置在其以弹簧锁的方式与子模块2和轴环4以弹簧锁方式接合时进行径向收缩。当使用夹持装置以便使子模块和锁定凸缘接合时,底部凸缘14锁定在子模块凸缘6上方,顶部凸缘13以支承方式与唇部8接合。另外,轴环4具有一个用于与顶部凸缘13进行锁定接合的梯状支座15。Figures 4a, 4b and 5 show a preferred embodiment of the holding
图4c示出夹持装置7的一个替代实施例。该实施例具有附加的突出物41,有助于以手动方式将夹持装置7从子模块2和轴环4上拆下。附加的突出物41沿径向从夹持装置7的侧壁12并在侧壁12裂口的两侧上延伸。FIG. 4 c shows an alternative embodiment of the
图7a-c以及图8a-c示出子模块连接套管5的实施例。这些视图示出凸缘6的细节和连接套管5的O形圈支座通道17的特征。凸缘6的一侧18用于与轴环4支承接合,第二侧19用于与夹持装置7锁定接合。另外,图7a-c所示的子模块连接套管5的实施例具有一个用作O形圈支座的管道17,同时图8a-c所示的子模块连接套管5的实施例具有两个用作O形圈支座的管道17。Figures 7a-c and Figures 8a-c show an embodiment of a
管1还可包括一个可拆卸的罩帽,用于与外壳进行气密性的密封接合。图9a和9b示出该罩帽的最佳实施例,其中该罩帽包括一个圆盘21,该圆盘上沿轴向延伸的螺纹轴22沿中心安装在一侧。该圆盘21同样在另一侧具有突出物23,以方便手动旋转罩帽20。该罩帽将在以下进行详细描述。Tube 1 may also include a removable cap for hermetically sealed engagement with the housing. Figures 9a and 9b show a preferred embodiment of the cap, wherein the cap comprises a disc 21 on which an axially extending threaded shaft 22 is centrally mounted on one side. This disc 21 also has a
一个径向间隔的凸缘24在罩帽与上述轴22相同的一侧上从罩帽20沿轴向向外延伸。该凸缘允许罩帽20与外壳1形成气密性的密封接合。图10示出罩帽20在使用时的最佳实施例。A radially spaced flange 24 extends axially outwardly from the
在如图11所示本发明的另一实施例中,一个薄膜过滤装置25包括一个顶部元件26和一个基部元件27,其中每个过滤装置都是上述薄膜过滤管的一个实施例并且与四个薄膜过滤子模块2相连。每个顶部元件26与滤出液管道28相连,以便在每个顶部元件26和滤出液管道28之间实现流体连通。在薄膜过滤管1用作顶部元件26时不再需要罩帽20。不需要罩帽20能允许在管1和滤出液管道28之间实现流体连通。In another embodiment of the present invention as shown in Figure 11, a
另外,特别在图12a和12b中示出,每个基部元件27与一个清洗液管道11相连,以便在每个基部元件27和清洗液管道11之间实现流体连通。在薄膜过滤管1用作基部元件27时,罩帽20的螺纹轴22以螺纹方式与清洗液管道11上的一个相应孔相接合。同样,在最佳实施例中,也不再需要夹持装置7来将子模块2锁定在基部元件上。这是因为子模块2将或者通过重力或者利用固定在其顶部元件26内合适位置的子模块顶部和夹持装置7,而固定在基部元件27的相应轴环4内。Furthermore, as shown in particular in FIGS. 12 a and 12 b , each
在本发明的一个替代实施例中,上述轴22是中空的并具有一个内部螺纹部分。在该实施例中,轴22不是以螺纹方式与清洗液管道上的孔接合,而是以内部螺纹方式与一个从清洗液管道11垂直突出的配合轴相接合。In an alternative embodiment of the invention, said shaft 22 is hollow and has an internally threaded portion. In this embodiment, the shaft 22 is not threadedly engaged with a hole in the cleaning fluid conduit, but is internally threaded with a mating shaft protruding perpendicularly from the cleaning
在本发明的另一实施例中,一个薄膜过滤装置排29包括若干上述薄膜过滤装置25,其中每个顶部元件与滤出液管道28相连,每个基部元件27与清洗液管道11相连。如图11所示,也可在其之间设置加强元件30,这样可有助于过滤系统的物理稳定性。典型地,在每个装置排29中有八个布置在一个垂直位置上的薄膜过滤装置25。当应用在一个过滤系统中时,装置排29基本浸入物料中,在此物料包含在一个具有开口顶部的箱31中。In another embodiment of the present invention, a
最好,空气用作流经清洗液管道11的过滤子模块清洗液,。图11、12a和12b很好地示出,清洗液管道11基本在基部元件27的上方,并布置在一条位于轴环4之间并沿装置排29长度的直线上。这就允许清洗液管道11通过若干位于其下侧的通道10为基部元件27供应空气。通过清洗液管道11下侧为基部元件27供应空气使得可控制地释放清洗空气,保证了沿装置排29的整个长度均匀地进行分配。Preferably, air is used as the filtered submodule cleaning fluid flowing through the cleaning
在本发明的另一实施例中,过滤系统包括一个薄膜过滤装置阵列,如图11和13所示包括若干薄膜过滤装置排29,其中每个滤出液管道28连接在一系列滤出液管道32上。In another embodiment of the present invention, the filtration system includes an array of membrane filtration devices, as shown in Figures 11 and 13, including several membrane
过滤装置排29另外还适于相对容易地从薄膜过滤装置阵列上拆下。当拆卸时,过滤装置排可以通过垂直地从该阵列上提升该装置排而从阵列上卸下。相似地,装置排也可以通过垂直地将装置排放进预定位置上而逐个地放置进阵列中。这样就使阵列的装卸变得更容易并且能更方便地接触到放置在阵列中心或靠近中心的子模块。
根据本发明的另一方面,提供了一个薄膜过滤装置阵列队,如图15所示包括若干图14所示的薄膜过滤装置阵列,其中滤出液管道阵列32通过管道阵列队33而连接,这样滤出液管道阵列32与管道阵列队33实现流体连接。According to another aspect of the present invention, a membrane filtration device array team is provided, as shown in Figure 15, comprises several membrane filtration device arrays shown in Figure 14, wherein filtrate pipeline array 32 is connected by pipeline array team 33, like this The filtrate pipeline array 32 is in fluid connection with the pipeline array team 33.
在过滤过程中,箱体31基本上连续地被填满物料,该物料依次将过滤子模块2的阵列浸没住。泵34通过从过滤子模块2抽取物料而生成滤出液。泵34所抽取出的负压下的滤出液,穿过管1,通过滤出液管道28、滤出液管道阵列32以及滤出液管道阵列队33并到达泵。滤出液随后离开泵,同时也通过一滤出液出口管道35而离开过滤系统。During the filtration process, the tank 31 is substantially continuously filled with material which in turn submerges the array of
尽管已经通过特定实例以及使用在对大气开放的过滤系统中的过滤管对本发明进行了描述,但是本领域技术人员能理解到本发明可以实现,以许多其它形式,包括使用在与大气相密闭的过滤系统中的过滤管。Although the invention has been described in terms of specific examples and use of a filter tube in a filter system open to the atmosphere, those skilled in the art will appreciate that the invention can be practiced in many other forms, including use in a filter tube closed to the atmosphere Filter tubes in the filter system.
Claims (30)
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| AUPP9850 | 1999-04-20 | ||
| AUPP9850A AUPP985099A0 (en) | 1999-04-20 | 1999-04-20 | Membrane filtration manifold system |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1347338A CN1347338A (en) | 2002-05-01 |
| CN1224449C true CN1224449C (en) | 2005-10-26 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
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| CNB008064695A Expired - Lifetime CN1224449C (en) | 1999-04-20 | 2000-04-20 | Membrane filtration manifold system |
Country Status (11)
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|---|---|
| US (2) | US20020148767A1 (en) |
| EP (1) | EP1189682B1 (en) |
| JP (1) | JP4533539B2 (en) |
| KR (1) | KR100664619B1 (en) |
| CN (1) | CN1224449C (en) |
| AT (1) | ATE485883T1 (en) |
| AU (1) | AUPP985099A0 (en) |
| DE (1) | DE60045155D1 (en) |
| ES (1) | ES2354409T3 (en) |
| NZ (1) | NZ514482A (en) |
| WO (1) | WO2000062908A1 (en) |
Families Citing this family (76)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0952885B1 (en) | 1996-12-20 | 2010-09-22 | Siemens Water Technologies Corp. | Scouring method |
| US6641733B2 (en) | 1998-09-25 | 2003-11-04 | U. S. Filter Wastewater Group, Inc. | Apparatus and method for cleaning membrane filtration modules |
| AUPP985099A0 (en) | 1999-04-20 | 1999-05-13 | Usf Filtration And Separations Group Inc. | Membrane filtration manifold system |
| AUPQ680100A0 (en) | 2000-04-10 | 2000-05-11 | Usf Filtration And Separations Group Inc. | Hollow fibre restraining system |
| AUPR064800A0 (en) | 2000-10-09 | 2000-11-02 | Usf Filtration And Separations Group Inc. | Improved membrane filtration system |
| AUPR143400A0 (en) | 2000-11-13 | 2000-12-07 | Usf Filtration And Separations Group Inc. | Modified membranes |
| AUPR421501A0 (en) | 2001-04-04 | 2001-05-03 | U.S. Filter Wastewater Group, Inc. | Potting method |
| AUPR584301A0 (en) | 2001-06-20 | 2001-07-12 | U.S. Filter Wastewater Group, Inc. | Membrane polymer compositions |
| AUPR692401A0 (en) | 2001-08-09 | 2001-08-30 | U.S. Filter Wastewater Group, Inc. | Method of cleaning membrane modules |
| AUPR774201A0 (en) | 2001-09-18 | 2001-10-11 | U.S. Filter Wastewater Group, Inc. | High solids module |
| DE60213184T2 (en) | 2001-11-16 | 2007-06-28 | U.S. Filter Wastewater Group, Inc. | Method for cleaning membranes |
| US7247238B2 (en) | 2002-02-12 | 2007-07-24 | Siemens Water Technologies Corp. | Poly(ethylene chlorotrifluoroethylene) membranes |
| AUPS300602A0 (en) | 2002-06-18 | 2002-07-11 | U.S. Filter Wastewater Group, Inc. | Methods of minimising the effect of integrity loss in hollow fibre membrane modules |
| JP4282598B2 (en) | 2002-10-10 | 2009-06-24 | シーメンス・ウォーター・テクノロジーズ・コーポレーション | Filtration device and method for cleaning the filtration device |
| AU2002953111A0 (en) | 2002-12-05 | 2002-12-19 | U. S. Filter Wastewater Group, Inc. | Mixing chamber |
| ES2308159T3 (en) * | 2003-03-05 | 2008-12-01 | Hydranautics | SUBMERSIBLE MEMBRANE MODULAR FILTRATION DEVICE THAT HAS REPLACABLE MEMBRANE ELEMENTS. |
| AU2003903507A0 (en) | 2003-07-08 | 2003-07-24 | U. S. Filter Wastewater Group, Inc. | Membrane post-treatment |
| US8268176B2 (en) | 2003-08-29 | 2012-09-18 | Siemens Industry, Inc. | Backwash |
| KR20070003783A (en) | 2003-11-14 | 2007-01-05 | 유.에스. 필터 웨이스트워터 그룹, 인크. | Improved Module Cleaning Method |
| US8758621B2 (en) | 2004-03-26 | 2014-06-24 | Evoqua Water Technologies Llc | Process and apparatus for purifying impure water using microfiltration or ultrafiltration in combination with reverse osmosis |
| AU2005240524C1 (en) | 2004-04-22 | 2009-12-24 | Evoqua Water Technologies Llc | Filtration apparatus comprising a membrane bioreactor and a treatment vessel for digesting organic materials |
| WO2005118115A1 (en) * | 2004-05-26 | 2005-12-15 | Trisep Corporation | Network for supporting spiral wound membrane cartridges for submerged operation |
| JP2008504122A (en) | 2004-07-02 | 2008-02-14 | シーメンス・ウォーター・テクノロジーズ・コーポレーション | Gas transport membrane |
| JP2008505197A (en) | 2004-07-05 | 2008-02-21 | シーメンス・ウォーター・テクノロジーズ・コーポレーション | Hydrophilic membrane |
| NZ588094A (en) | 2004-08-20 | 2012-04-27 | Siemens Water Tech Corp | Potting head for hollow fibre filter module |
| CN101043933B (en) | 2004-09-07 | 2012-09-05 | 西门子工业公司 | Reduction of backwash liquid waste |
| NZ553742A (en) | 2004-09-14 | 2010-09-30 | Siemens Water Tech Corp | Methods and apparatus for removing solids from a membrane module |
| US8377305B2 (en) | 2004-09-15 | 2013-02-19 | Siemens Industry, Inc. | Continuously variable aeration |
| US7591950B2 (en) | 2004-11-02 | 2009-09-22 | Siemens Water Technologies Corp. | Submerged cross-flow filtration |
| CN101084057B (en) | 2004-12-03 | 2013-10-23 | 西门子工业公司 | Membrane post treatment |
| EP1838422A4 (en) | 2004-12-24 | 2009-09-02 | Siemens Water Tech Corp | Simple gas scouring method and apparatus |
| AU2005318930B2 (en) | 2004-12-24 | 2010-06-03 | Evoqua Water Technologies Llc | Cleaning in membrane filtration systems |
| US20060180548A1 (en) * | 2005-02-17 | 2006-08-17 | Zhenghua Ji | Liquid depletion in solid phase separation processes |
| WO2006116797A1 (en) | 2005-04-29 | 2006-11-09 | Siemens Water Technologies Corp. | Chemical clean for membrane filter |
| JP2009500169A (en) | 2005-07-14 | 2009-01-08 | シーメンス・ウォーター・テクノロジーズ・コーポレーション | Monopersulfate treatment of membranes |
| SG140229A1 (en) | 2005-08-22 | 2008-03-28 | Siemens Water Tech Corp | An assembly for water filtration using a tube manifold to minimise backwash |
| US7563363B2 (en) | 2005-10-05 | 2009-07-21 | Siemens Water Technologies Corp. | System for treating wastewater |
| WO2007044415A2 (en) | 2005-10-05 | 2007-04-19 | Siemens Water Technologies Corp. | Method and apparatus for treating wastewater |
| WO2007051209A2 (en) * | 2005-10-28 | 2007-05-03 | Dual Vortex Microfiltration, Llc | System and method of fluid filtration utilizing cross-flow currents |
| US7455765B2 (en) | 2006-01-25 | 2008-11-25 | Siemens Water Technologies Corp. | Wastewater treatment system and method |
| WO2008051546A2 (en) | 2006-10-24 | 2008-05-02 | Siemens Water Technologies Corp. | Infiltration/inflow control for membrane bioreactor |
| US20100219130A1 (en) * | 2006-10-30 | 2010-09-02 | Kopp Clinton V | System and Method of Fluid Filtration Utilizing Cross-Flow Currents |
| WO2008123972A1 (en) | 2007-04-02 | 2008-10-16 | Siemens Water Technologies Corp. | Improved infiltration/inflow control for membrane bioreactor |
| US9764288B2 (en) | 2007-04-04 | 2017-09-19 | Evoqua Water Technologies Llc | Membrane module protection |
| KR20160045152A (en) | 2007-05-29 | 2016-04-26 | 에보쿠아 워터 테크놀로지스 엘엘씨 | Water treatment system |
| ES2429448T3 (en) | 2008-01-31 | 2013-11-14 | Toray Industries, Inc. | Hollow fiber membrane filtration apparatus |
| US8568589B2 (en) * | 2008-02-25 | 2013-10-29 | Nitto Denko Corporation | Connection member and separation membrane module using the same |
| US20100125235A1 (en) * | 2008-06-16 | 2010-05-20 | Triaxis Medical Devices, Inc. | Blood Treatment Apparatus Having Branched Flow Distribution |
| EP2331242B1 (en) | 2008-07-24 | 2018-09-05 | Evoqua Water Technologies LLC | Frame system for membrane filtration modules |
| KR20110044312A (en) | 2008-08-20 | 2011-04-28 | 지멘스 워터 테크놀로지스 코포레이션 | Improved backwash energy efficiency of membrane systems |
| KR101506034B1 (en) * | 2008-09-29 | 2015-03-26 | 코오롱인더스트리 주식회사 | Alignment device of pressurized module and filtration system including the same |
| AU2010101488B4 (en) | 2009-06-11 | 2013-05-02 | Evoqua Water Technologies Llc | Methods for cleaning a porous polymeric membrane and a kit for cleaning a porous polymeric membrane |
| NL2003669C2 (en) * | 2009-10-19 | 2011-04-20 | X Flow Bv | Apparatus and process for the separation of particulate matter from a fluid. |
| HUE045642T2 (en) | 2010-04-30 | 2020-01-28 | Evoqua Water Tech Llc | Fluid flow distribution device |
| CN103118766B (en) | 2010-09-24 | 2016-04-13 | 伊沃夸水处理技术有限责任公司 | Fluid Control Manifolds for Membrane Filtration Systems |
| CA2850309C (en) | 2011-09-30 | 2020-01-07 | Evoqua Water Technologies Llc | Improved manifold arrangement |
| CA2850522C (en) | 2011-09-30 | 2021-03-16 | Evoqua Water Technologies Llc | Shut-off valve for isolation of hollow fiber membrane filtration module |
| WO2013113833A1 (en) * | 2012-02-03 | 2013-08-08 | Intewa Gmbh | Filter station |
| CN104394965B (en) | 2012-06-28 | 2016-11-23 | 伊沃夸水处理技术有限责任公司 | encapsulating method |
| KR20150054918A (en) | 2012-09-14 | 2015-05-20 | 에보쿠아 워터 테크놀로지스 엘엘씨 | A polymer blend for membranes |
| DE112013004713T5 (en) | 2012-09-26 | 2015-07-23 | Evoqua Water Technologies Llc | Membrane safety device |
| AU2013231145B2 (en) | 2012-09-26 | 2017-08-17 | Evoqua Water Technologies Llc | Membrane potting methods |
| AU2013323934A1 (en) | 2012-09-27 | 2015-02-26 | Evoqua Water Technologies Llc | Gas scouring apparatus for immersed membranes |
| BR112015020328B1 (en) | 2013-02-28 | 2022-05-31 | Sorrento Therapeutics, Inc | Transdermal drug delivery device |
| AU350360S (en) * | 2013-07-10 | 2013-08-26 | Evoqua Water Tech Llc | Filtration components |
| DE102013214090A1 (en) * | 2013-07-18 | 2015-01-22 | Mahle International Gmbh | Cross-flow filter for wine |
| HUE061765T2 (en) | 2013-10-02 | 2023-08-28 | Rohm & Haas Electronic Mat Singapore Pte Ltd | Device for repairing a membrane filtration module |
| USD764018S1 (en) * | 2013-12-18 | 2016-08-16 | Evoqua Water Technologies Llc | Filtration header |
| MX383552B (en) | 2014-12-22 | 2025-03-14 | Pro Equipment Inc | HIGH SPEED CROSS FLOW DYNAMIC MEMBRANE FILTER. |
| WO2017011068A1 (en) | 2015-07-14 | 2017-01-19 | Evoqua Water Technologies Llc | Aeration device for filtration system |
| EP3538242B1 (en) * | 2016-11-08 | 2024-10-30 | Pentair Filtration Solutions, LLC | Particle separation system |
| NO345138B1 (en) | 2018-11-30 | 2020-10-12 | Aker Solutions As | A filter device, and method of assembly |
| JP7470691B2 (en) * | 2018-12-12 | 2024-04-18 | アクアポリン エーエス | Hollow Fiber Module |
| EP3967389B1 (en) * | 2019-10-15 | 2024-12-18 | Hainan Litree Purifying Technology Co., Ltd | External pressure type hollow fiber membrane component, filtration membrane component, and membrane filtration module |
| KR20210132921A (en) * | 2020-04-28 | 2021-11-05 | 주식회사 아모그린텍 | filter module for water-purifying device using gravity and water-purifying device including the same |
| US11331616B2 (en) * | 2020-09-25 | 2022-05-17 | Mark Henderson | Pool filter assembly |
Family Cites Families (200)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US400890A (en) * | 1889-04-09 | Regulation of electric motors | ||
| US75504A (en) * | 1868-03-10 | Improved pavement | ||
| US226797A (en) * | 1880-04-20 | Elias h | ||
| US178365A (en) * | 1876-06-06 | Improvement in washing-machines | ||
| US205519A (en) * | 1878-07-02 | Improvement in file-guards | ||
| US148767A (en) * | 1874-03-17 | Improvement in making butterime | ||
| US396726A (en) * | 1889-01-29 | Car coupling-link | ||
| US478913A (en) * | 1892-07-12 | Sack-holder | ||
| US141248A (en) * | 1873-07-29 | Improvement in the methods of blasting rock | ||
| US27951A (en) * | 1860-04-17 | Improvement in windmills | ||
| US136746A (en) * | 1873-03-11 | Improvement in combined globe-valves and traps | ||
| US164332A (en) * | 1875-06-08 | Improvement in nail-feed attachments for nailing-machines | ||
| US89659A (en) * | 1869-05-04 | Improvement in nut-locks for fish-plates | ||
| US153299A (en) * | 1874-07-21 | Improvement in edge-planes | ||
| US763612A (en) * | 1903-08-07 | 1904-06-28 | Charles W Joynt | Portable apparatus for thawing frozen ground. |
| NL269380A (en) * | 1960-09-19 | |||
| US3693406A (en) | 1970-01-26 | 1972-09-26 | Air Intake Renu | Method for inspecting filters |
| US3708071A (en) * | 1970-08-05 | 1973-01-02 | Abcor Inc | Hollow fiber membrane device and method of fabricating same |
| US3992301A (en) | 1973-11-19 | 1976-11-16 | Raypak, Inc. | Automatic flushing system for membrane separation machines such as reverse osmosis machines |
| US3968192A (en) * | 1974-04-19 | 1976-07-06 | The Dow Chemical Company | Method of repairing leaky hollow fiber permeability separatory devices |
| US4192750A (en) * | 1976-08-09 | 1980-03-11 | Massey-Ferguson Inc. | Stackable filter head unit |
| US4107043A (en) * | 1977-03-03 | 1978-08-15 | Creative Dispensing Systems, Inc. | Inlet conduit fluid filter |
| US4192780A (en) * | 1977-12-02 | 1980-03-11 | Exxon Research & Engineering Co. | Method of making lead-rich and bismuth-rich pyrochlore compounds using an alkaline medium and a reaction enhancing anodic potential |
| US4193780A (en) | 1978-03-20 | 1980-03-18 | Industrial Air, Inc. | Air filter construction |
| US4188817A (en) * | 1978-10-04 | 1980-02-19 | Standard Oil Company (Indiana) | Method for detecting membrane leakage |
| US4218324A (en) * | 1979-05-03 | 1980-08-19 | Textron, Inc. | Filter element having removable filter media member |
| US4248648A (en) * | 1979-07-18 | 1981-02-03 | Baxter Travenol Laboratories, Inc. | Method of repairing leaks in a hollow capillary fiber diffusion device |
| JPS5770144A (en) * | 1980-10-17 | 1982-04-30 | Asahi Glass Co Ltd | Organic solution of fluorinated copolymer containing carboxyl group |
| US4384474A (en) * | 1980-10-30 | 1983-05-24 | Amf Incorporated | Method and apparatus for testing and using membrane filters in an on site of use housing |
| JPS57102202A (en) * | 1980-12-18 | 1982-06-25 | Toyobo Co Ltd | Fluid separator |
| JPS624408Y2 (en) | 1981-04-20 | 1987-01-31 | ||
| JPS5888007A (en) | 1981-11-20 | 1983-05-26 | Asahi Glass Co Ltd | How to separate liquid mixtures |
| US4812235A (en) * | 1982-03-29 | 1989-03-14 | Hr Textron, Inc. | Filter element assembly replaceable mesh pack |
| US4540490A (en) | 1982-04-23 | 1985-09-10 | Jgc Corporation | Apparatus for filtration of a suspension |
| WO1983003984A1 (en) * | 1982-05-13 | 1983-11-24 | Gerhard Kunz | Method for the treatment of a liquid phase, particularly method for desalting aqueous solutions, as well as device for its implementation |
| JPS5952507A (en) * | 1982-06-03 | 1984-03-27 | デ−・エル・エム・ドクトル・ミユラ−・アクチエンゲゼルシヤフト | Apparatus for continuously concentrating suspension |
| GB2132366B (en) | 1982-12-27 | 1987-04-08 | Brunswick Corp | Method and device for testing the permeability of membrane filters |
| CA1221645A (en) | 1983-02-28 | 1987-05-12 | Yoshihiro Okano | Filtration apparatus using hollow fiber-membrane |
| JPS59160511A (en) * | 1983-02-28 | 1984-09-11 | Kuraray Co Ltd | Filter device |
| DE3317396A1 (en) * | 1983-05-13 | 1984-11-15 | Henkel KGaA, 4000 Düsseldorf | USE OF COLOYERS FROM ESTERS AND AMIDES OF ACRYLIC AND / OR METHACRYLIC ACIDS AS STOCK POINTS LOW FOR PARAFFIN SOLUTIONS |
| GB8313635D0 (en) * | 1983-05-17 | 1983-06-22 | Whatman Reeve Angel Plc | Porosimeter |
| JPS6017204U (en) * | 1983-07-11 | 1985-02-05 | 日東電工株式会社 | Fluid separation device fittings |
| US4636296A (en) * | 1983-08-18 | 1987-01-13 | Gerhard Kunz | Process and apparatus for treatment of fluids, particularly desalinization of aqueous solutions |
| US4650586A (en) | 1983-09-26 | 1987-03-17 | Kinetico, Inc. | Fluid treatment system |
| US4756875A (en) * | 1983-09-29 | 1988-07-12 | Kabushiki Kaisha Toshiba | Apparatus for filtering water containing radioactive substances in nuclear power plants |
| WO1985001449A1 (en) | 1983-09-30 | 1985-04-11 | Memtec Limited | Cleaning of filters |
| JPS60136950U (en) | 1984-02-23 | 1985-09-11 | 株式会社吉野工業所 | liquid spout |
| US4609465A (en) | 1984-05-21 | 1986-09-02 | Pall Corporation | Filter cartridge with a connector seal |
| EP0170895B1 (en) | 1984-07-09 | 1989-03-22 | Millipore Corporation | Improved electrodeionization apparatus and method |
| JPS6125903U (en) * | 1984-07-24 | 1986-02-15 | 株式会社 伊藤鉄工所 | filtration equipment |
| DE3428307A1 (en) | 1984-08-01 | 1986-02-13 | Filterwerk Mann & Hummel Gmbh, 7140 Ludwigsburg | DISPLAY DEVICE FOR THE POLLUTION LEVEL OF SUCTION AIR FILTERS |
| JPS6197006U (en) | 1984-11-30 | 1986-06-21 | ||
| JPS61107905U (en) | 1984-12-19 | 1986-07-09 | ||
| US4931186A (en) * | 1985-03-05 | 1990-06-05 | Memtec Limited | Concentration of solids in a suspension |
| US5024762A (en) * | 1985-03-05 | 1991-06-18 | Memtec Limited | Concentration of solids in a suspension |
| US4642182A (en) * | 1985-03-07 | 1987-02-10 | Mordeki Drori | Multiple-disc type filter with extensible support |
| US4816160A (en) * | 1985-03-28 | 1989-03-28 | Memtec Limited | Cooling hollow fibre cross-flow separators |
| US4793932A (en) | 1985-04-10 | 1988-12-27 | Memtec Limited | Variable volume filter or concentrator |
| CA1247329A (en) * | 1985-05-06 | 1988-12-28 | Craig J. Brown | Fluid treatment process and apparatus |
| JPS61257203A (en) | 1985-05-10 | 1986-11-14 | Terumo Corp | Hydrophilic porous membrane and its preparation |
| JPS61263605A (en) | 1985-05-17 | 1986-11-21 | Toshiba Corp | Hollow yarn membrane device |
| JPS61192309U (en) | 1985-05-24 | 1986-11-29 | ||
| US4660411A (en) * | 1985-05-31 | 1987-04-28 | Reid Philip L | Apparatus for measuring transmission of volatile substances through films |
| US4656865A (en) * | 1985-09-09 | 1987-04-14 | The Dow Chemical Company | System for analyzing permeation of a gas or vapor through a film or membrane |
| US4876006A (en) | 1985-10-08 | 1989-10-24 | Ebara Corporation | Hollow fiber filter device |
| US4695553A (en) | 1985-11-01 | 1987-09-22 | Becton Dickinson And Co., Inc. | Method for increasing agglutination of groups of cells to produce improved cell layer interface in centrifuged blood sample using antibodies |
| DE3546091A1 (en) * | 1985-12-24 | 1987-07-02 | Kernforschungsz Karlsruhe | CROSS-CURRENT MICROFILTER |
| JPH0319928Y2 (en) | 1986-01-06 | 1991-04-26 | ||
| US4779448A (en) | 1986-01-28 | 1988-10-25 | Donaldson Company, Inc. | Photoelectric bubble detector apparatus and method |
| JPS62140607U (en) | 1986-02-27 | 1987-09-04 | ||
| JPH0742861B2 (en) | 1986-03-10 | 1995-05-15 | ヤマハ発動機株式会社 | Internal combustion engine intake system |
| JPS62179540U (en) | 1986-05-01 | 1987-11-14 | ||
| DE3617724A1 (en) * | 1986-05-27 | 1987-12-03 | Akzo Gmbh | METHOD FOR DETERMINING THE BLOW POINT OR THE BIGGEST PORE OF MEMBRANES OR FILTER MATERIALS |
| FR2600265B1 (en) * | 1986-06-20 | 1991-09-06 | Rhone Poulenc Rech | DRY AND HYDROPHILIC SEMI-PERMEABLE MEMBRANES BASED ON VINYLIDENE POLYFLUORIDE |
| JPH07770Y2 (en) | 1986-07-07 | 1995-01-11 | スズキ株式会社 | Vehicle speed change control device |
| US4839048A (en) * | 1986-07-08 | 1989-06-13 | Pall Corporation | Container for pressurized fluid |
| US4670145A (en) * | 1986-07-08 | 1987-06-02 | E. I. Du Pont De Nemours And Company | Multiple bundle fluid separation apparatus |
| ES2014516A6 (en) * | 1986-07-11 | 1990-07-16 | Mentec Ltd | Cleaning of filters. |
| JPH01501046A (en) * | 1986-09-04 | 1989-04-13 | メムテック・リミテッド | How to clean hollow fiber filters |
| US4876012A (en) * | 1986-09-12 | 1989-10-24 | Memtec Limited | Hollow fibre filter cartridge and header |
| US5094750A (en) * | 1986-09-12 | 1992-03-10 | Memtec Limited | Hollow fibre filter cartridge and header |
| JPH0328797Y2 (en) | 1986-11-06 | 1991-06-20 | ||
| JPS6397634U (en) | 1986-12-16 | 1988-06-24 | ||
| US4781831A (en) | 1986-12-19 | 1988-11-01 | Goldsmith Robert L | Cross-flow filtration device with filtrate flow conduits and method of forming same |
| JPS63143905U (en) | 1987-03-09 | 1988-09-21 | ||
| JPH01503265A (en) * | 1987-04-02 | 1989-11-02 | モトローラ・インコーポレーテッド | Antenna tuning device for small personal communication devices |
| JPH0671120B2 (en) | 1987-04-21 | 1994-09-07 | 日本電気株式会社 | Optical integrated device |
| JPS63180254U (en) | 1987-05-14 | 1988-11-21 | ||
| US4846970A (en) * | 1987-06-22 | 1989-07-11 | Osmonics, Inc. | Cross-flow filtration membrane test unit |
| US4784771A (en) | 1987-08-03 | 1988-11-15 | Environmental Water Technology, Inc. | Method and apparatus for purifying fluids |
| US5221478A (en) * | 1988-02-05 | 1993-06-22 | The Dow Chemical Company | Chromatographic separation using ion-exchange resins |
| JP2527462B2 (en) | 1988-06-03 | 1996-08-21 | ダイセル化学工業株式会社 | Hollow fiber ultrafiltration membrane module automatic leak detection and alarm system |
| GB8816216D0 (en) | 1988-07-07 | 1988-08-10 | Fairey Arlon Ltd | Filters |
| JPH0671540B2 (en) | 1988-12-20 | 1994-09-14 | 株式会社東芝 | Cleaning method of hollow fiber membrane filter |
| US4999038A (en) | 1989-02-07 | 1991-03-12 | Lundberg Bo E H | Filter unit |
| DE3904544A1 (en) | 1989-02-15 | 1990-08-16 | Fraunhofer Ges Forschung | POLYMINE MEMBRANES BASED ON POLYVINYLIDENE FLUORIDE, METHOD FOR THE PRODUCTION AND USE THEREOF |
| JP2773231B2 (en) | 1989-04-25 | 1998-07-09 | 東洋紡績株式会社 | Leak test method for hydrophobic hollow fiber type porous membrane |
| NL8901090A (en) | 1989-04-28 | 1990-11-16 | X Flow Bv | METHOD FOR MANUFACTURING A MICROPOROUS MEMBRANE AND SUCH MEMBRANE |
| US5005430A (en) * | 1989-05-16 | 1991-04-09 | Electric Power Research Institute, Inc. | Automated membrane filter sampler |
| US5138870A (en) | 1989-07-10 | 1992-08-18 | Lyssy Georges H | Apparatus for measuring water vapor permeability through sheet materials |
| DE3923128A1 (en) | 1989-07-13 | 1991-01-24 | Akzo Gmbh | FLAX OR CAPILLARY MEMBRANE BASED ON A HOMOGENEOUS MIXTURE OF POLYVINYLIDE FLUORIDE AND OF A SECOND, BY CHEMICAL IMPROVEMENT, HYDROPHILIBLABLE POLYMERS |
| WO1991004783A1 (en) * | 1989-09-29 | 1991-04-18 | Memtec Limited | Filter cartridge manifold |
| US5227063A (en) * | 1989-10-03 | 1993-07-13 | Zenon Environmental Inc. | Tubular membrane module |
| US5079272A (en) * | 1989-11-30 | 1992-01-07 | Millipore Corporation | Porous membrane formed from interpenetrating polymer network having hydrophilic surface |
| US5158721A (en) | 1989-11-30 | 1992-10-27 | Millipore Corporation | Porous membrane formed from interpenetrating polymer network having hydrophilic surface |
| US4990038A (en) * | 1990-01-29 | 1991-02-05 | G & H Technology, Inc. | Rotationally and axially restrained drill bit and chuck assembly |
| US5066375A (en) | 1990-03-19 | 1991-11-19 | Ionics, Incorporated | Introducing and removing ion-exchange and other particulates from an assembled electrodeionization stack |
| EP0525096B1 (en) * | 1990-04-20 | 1998-10-21 | Memtec Limited | Modular microporous filter assemblies |
| JPH0810585Y2 (en) | 1990-05-22 | 1996-03-29 | 大成建設株式会社 | Lifting machine |
| US5364527A (en) | 1990-06-20 | 1994-11-15 | Heinz Zimmermann | Apparatus and process for treating water |
| DE4117281C2 (en) | 1990-06-29 | 1996-02-22 | Gore Enterprise Holdings Inc | Hydrophilized, microporous membrane made of polytetrafluoroethylene and process for its production |
| US5104546A (en) * | 1990-07-03 | 1992-04-14 | Aluminum Company Of America | Pyrogens separations by ceramic ultrafiltration |
| US5639373A (en) * | 1995-08-11 | 1997-06-17 | Zenon Environmental Inc. | Vertical skein of hollow fiber membranes and method of maintaining clean fiber surfaces while filtering a substrate to withdraw a permeate |
| US5104535A (en) * | 1990-08-17 | 1992-04-14 | Zenon Environmental, Inc. | Frameless array of hollow fiber membranes and module containing a stack of arrays |
| US5182019A (en) * | 1990-08-17 | 1993-01-26 | Zenon Environmental Inc. | Cartridge of hybrid frameless arrays of hollow fiber membranes and module containing an assembly of cartridges |
| US5248424A (en) | 1990-08-17 | 1993-09-28 | Zenon Environmental Inc. | Frameless array of hollow fiber membranes and method of maintaining clean fiber surfaces while filtering a substrate to withdraw a permeate |
| FR2666245B1 (en) | 1990-08-31 | 1992-10-23 | Lyonnaise Eaux | METHOD FOR CONTROLLING THE OPERATING MODES OF AN AUTOMATIC WATER FILTRATION APPARATUS ON TUBULAR MEMBRANES. |
| JP2904564B2 (en) * | 1990-08-31 | 1999-06-14 | オルガノ株式会社 | Method of scrubbing filtration tower using hollow fiber membrane |
| JP2858913B2 (en) | 1990-09-26 | 1999-02-17 | オルガノ株式会社 | Filtration method using hollow fiber membrane |
| USH1045H (en) | 1990-11-19 | 1992-05-05 | The United States Of America As Represented By The Secretary Of The Army | Air bubble leak detection test device |
| US5069065A (en) | 1991-01-16 | 1991-12-03 | Mobil Oil Corporation | Method for measuring wettability of porous rock |
| GB2253572B (en) | 1991-02-11 | 1994-12-14 | Aljac Engineering Limited | Flow device in fluid circuits |
| EP0510328B1 (en) * | 1991-03-07 | 1995-10-04 | Kubota Corporation | Apparatus for treating activated sludge |
| FR2674448B1 (en) | 1991-03-26 | 1994-03-25 | Dumez Lyonnaise Eaux | METHOD FOR CLEANING MESOPOROUS TUBULAR MEMBRANES OF ULTRAFILTRATION. |
| JP3093811B2 (en) | 1991-04-08 | 2000-10-03 | 旭化成工業株式会社 | Polyvinylidene fluoride resin film and method for producing the same |
| DE4117422C1 (en) | 1991-05-28 | 1992-11-12 | Willi Prof. Dr.-Ing. 7432 Bad Urach De Dettinger | Monitoring contamination level of filter, partic. for hydraulic fluids - in which signal is produced which correlates with quotient of two pressure differences and evaluating device produces signal to change filter when quotient reaches given value |
| DE4119040C2 (en) * | 1991-06-10 | 1997-01-02 | Pall Corp | Method and device for testing the operating state of filter elements |
| US5211823A (en) * | 1991-06-19 | 1993-05-18 | Millipore Corporation | Process for purifying resins utilizing bipolar interface |
| DE69230766T2 (en) | 1991-08-07 | 2000-08-31 | Usf Filtration Ltd., South Windsor | CONCENTRATION OF SOLIDS IN A SLUDGE USING CARBON FIBER MEMBRANES |
| US5137631A (en) | 1991-10-22 | 1992-08-11 | E. I. Du Pont De Nemours And Company | Multiple bundle permeator |
| JP3111101B2 (en) | 1991-12-03 | 2000-11-20 | 旭化成工業株式会社 | Leak inspection method for membrane separation equipment |
| US5198116A (en) * | 1992-02-10 | 1993-03-30 | D.W. Walker & Associates | Method and apparatus for measuring the fouling potential of membrane system feeds |
| WO1993015827A1 (en) * | 1992-02-12 | 1993-08-19 | Mitsubishi Rayon Co., Ltd. | Hollow yarn membrane module |
| DE69313574T2 (en) | 1992-05-01 | 1998-01-08 | Filtec Corp | Device for checking the integrity of membrane filters |
| JP2618820B2 (en) | 1992-05-18 | 1997-06-11 | ミンテック コーポレーション | Hollow fiber filter cartridge and manufacturing method |
| JP3250274B2 (en) * | 1992-10-08 | 2002-01-28 | 東レ株式会社 | Filter |
| JP2552863Y2 (en) * | 1992-10-22 | 1997-10-29 | エスエムシー株式会社 | Dehumidifier |
| AU663022B2 (en) * | 1992-11-02 | 1995-09-21 | Siemens Industry, Inc. | Fibre monitoring system |
| US5320760A (en) * | 1992-12-07 | 1994-06-14 | E. I. Du Pont De Nemours And Company | Method of determining filter pluggage by measuring pressures |
| US5401401A (en) * | 1993-01-13 | 1995-03-28 | Aquaria Inc. | Hang on tank canister filter |
| US5389260A (en) * | 1993-04-02 | 1995-02-14 | Clack Corporation | Brine seal for tubular filter |
| US5361625A (en) | 1993-04-29 | 1994-11-08 | Ylvisaker Jon A | Method and device for the measurement of barrier properties of films against gases |
| US5297420A (en) * | 1993-05-19 | 1994-03-29 | Mobil Oil Corporation | Apparatus and method for measuring relative permeability and capillary pressure of porous rock |
| FR2705734B1 (en) | 1993-05-25 | 1995-06-30 | Snecma | Method and device for improving the safety of fluid filters. |
| JPH06343837A (en) | 1993-06-02 | 1994-12-20 | Ebara Infilco Co Ltd | Hollow fiber membrane module |
| US5419816A (en) * | 1993-10-27 | 1995-05-30 | Halox Technologies Corporation | Electrolytic process and apparatus for the controlled oxidation of inorganic and organic species in aqueous solutions |
| FR2713220B1 (en) * | 1993-11-30 | 1996-03-08 | Omnium Traitement Valorisa | Installation of water purification with submerged filter membranes. |
| US5403479A (en) * | 1993-12-20 | 1995-04-04 | Zenon Environmental Inc. | In situ cleaning system for fouled membranes |
| JPH07185268A (en) | 1993-12-28 | 1995-07-25 | Toray Ind Inc | Hollow fiber filter membrane element and module |
| JP3486451B2 (en) | 1994-04-12 | 2004-01-13 | 三菱レイヨン株式会社 | Hollow fiber membrane module |
| US5531900A (en) * | 1994-07-07 | 1996-07-02 | University Of Arizona | Modification of polyvinylidene fluoride membrane and method of filtering |
| AUPM800694A0 (en) | 1994-09-09 | 1994-10-06 | Memtec Limited | Cleaning of hollow fibre membranes |
| US5470469A (en) | 1994-09-16 | 1995-11-28 | E. I. Du Pont De Nemours And Company | Hollow fiber cartridge |
| EP0814887B1 (en) * | 1995-03-15 | 2003-06-25 | USF Filtration and Separations Group Inc. | Filtration monitoring and control system |
| GB9511842D0 (en) * | 1995-06-10 | 1995-08-09 | North West Water Group Plc | Filter |
| US6685832B2 (en) | 1995-08-11 | 2004-02-03 | Zenon Environmental Inc. | Method of potting hollow fiber membranes |
| US6656356B2 (en) | 1998-10-09 | 2003-12-02 | Zenon Environmental Inc. | Aerated immersed membrane system |
| US5944997A (en) | 1995-08-11 | 1999-08-31 | Zenon Environmental Inc. | System for maintaining a clean skein of hollow fibers while filtering suspended solids |
| US6193890B1 (en) * | 1995-08-11 | 2001-02-27 | Zenon Environmental Inc. | System for maintaining a clean skein of hollow fibers while filtering suspended solids |
| DE69624492T2 (en) * | 1995-08-11 | 2003-06-26 | Zenon Environmental Inc., Oakville | VERTICAL STRAND OF HOLLOW FIBER MEMBRANES AND METHOD FOR MAINTAINING CLEAN FIBER SURFACES |
| JP3294979B2 (en) | 1995-09-14 | 2002-06-24 | 株式会社精工技研 | Optical fiber ferrule assembly with angle index indicating direction of polarization plane of optical fiber |
| JPH09141063A (en) | 1995-11-21 | 1997-06-03 | Mitsubishi Rayon Co Ltd | Hollow fiber membrane module |
| US5895570A (en) * | 1996-02-09 | 1999-04-20 | United States Filter Corporation | Modular filtering system |
| US6077435A (en) * | 1996-03-15 | 2000-06-20 | Usf Filtration And Separations Group Inc. | Filtration monitoring and control system |
| JPH10110657A (en) * | 1996-08-22 | 1998-04-28 | Stanadyne Automot Corp | Filter assembly having matching cartridge support structure |
| JP3686918B2 (en) | 1996-10-16 | 2005-08-24 | 森村興産株式会社 | Filtration device for solid-liquid separation of sewage, wastewater, etc. |
| USD396046S (en) | 1996-10-24 | 1998-07-14 | Allen Scheel | Steer device for an outboard motor |
| AUPO377796A0 (en) | 1996-11-21 | 1996-12-19 | Memtec America Corporation | Microporous membrane filtration and backwashing process |
| JP3436026B2 (en) | 1996-12-02 | 2003-08-11 | エヌオーケー株式会社 | Hollow fiber membrane module |
| JP3535945B2 (en) * | 1996-12-06 | 2004-06-07 | ヤマハ発動機株式会社 | Water purifier |
| AUPO412596A0 (en) * | 1996-12-10 | 1997-01-09 | Memtec America Corporation | Improved microporous membrane filtration assembly |
| EP0952885B1 (en) | 1996-12-20 | 2010-09-22 | Siemens Water Technologies Corp. | Scouring method |
| US6146747A (en) | 1997-01-22 | 2000-11-14 | Usf Filtration And Separations Group Inc. | Highly porous polyvinylidene difluoride membranes |
| USD396726S (en) | 1997-02-06 | 1998-08-04 | Abc Group | Combined air intake manifold and filter |
| JP3688092B2 (en) * | 1997-03-05 | 2005-08-24 | 株式会社三栄水栓製作所 | Pipe connection clip drop-off prevention structure |
| US6048454A (en) * | 1997-03-18 | 2000-04-11 | Jenkins; Dan | Oil filter pack and assembly |
| JP3684287B2 (en) * | 1997-03-19 | 2005-08-17 | 株式会社パイオラックス | Wiring and piping retaining clips |
| AUPO709797A0 (en) * | 1997-05-30 | 1997-06-26 | Usf Filtration And Separations Group Inc. | Predicting logarithmic reduction values |
| US5914039A (en) * | 1997-07-01 | 1999-06-22 | Zenon Environmental Inc. | Filtration membrane with calcined α-alumina particles therein |
| US6354444B1 (en) * | 1997-07-01 | 2002-03-12 | Zenon Environmental Inc. | Hollow fiber membrane and braided tubular support therefor |
| US6641733B2 (en) | 1998-09-25 | 2003-11-04 | U. S. Filter Wastewater Group, Inc. | Apparatus and method for cleaning membrane filtration modules |
| US6017451A (en) * | 1997-10-01 | 2000-01-25 | Kopf; Henry B. | Spider fitting for multi-module filter system, and motive cart assembly comprising same |
| US6083393A (en) * | 1997-10-27 | 2000-07-04 | Pall Corporation | Hydrophilic membrane |
| US6039872A (en) | 1997-10-27 | 2000-03-21 | Pall Corporation | Hydrophilic membrane |
| USD400890S (en) | 1997-12-03 | 1998-11-10 | Gambardella C Bruce | Automotive manifold |
| TWI222895B (en) * | 1998-09-25 | 2004-11-01 | Usf Filtration & Separations | Apparatus and method for cleaning membrane filtration modules |
| US6550747B2 (en) * | 1998-10-09 | 2003-04-22 | Zenon Environmental Inc. | Cyclic aeration system for submerged membrane modules |
| KR100439436B1 (en) * | 1998-10-09 | 2004-07-09 | 제논 인바이런멘탈 인코포레이티드 | Cyclic aeration system for submerged membrane modules |
| JP4107453B2 (en) * | 1998-11-26 | 2008-06-25 | 旭化成ケミカルズ株式会社 | Hollow fiber membrane cartridge |
| US6156200A (en) | 1998-12-08 | 2000-12-05 | Usf Filtration & Separations Group, Inc. | Gas-scrubbed hollow fiber membrane module |
| AUPP985099A0 (en) | 1999-04-20 | 1999-05-13 | Usf Filtration And Separations Group Inc. | Membrane filtration manifold system |
| HUP0105236A3 (en) | 1999-11-18 | 2006-05-29 | Zenon Environmental Inc Oakvil | Immersed membrane filtration system and overflow process |
| USD478913S1 (en) | 2000-02-24 | 2003-08-26 | Usf Filtration And Separations Group, Inc. | Manifold header |
| US6440303B2 (en) | 2000-03-02 | 2002-08-27 | Chapin Manufacturing, Inc. | Fluid filter |
| EP1423338B1 (en) | 2000-03-08 | 2007-01-24 | Zenon Technology Partnership | Reaktor with membrane module for gas transfer and membrane supported biofilm process |
| AUPQ680100A0 (en) | 2000-04-10 | 2000-05-11 | Usf Filtration And Separations Group Inc. | Hollow fibre restraining system |
| AU142387S (en) | 2000-05-31 | 2000-11-27 | Evoqua Water Tech Llc | Manifold header cap |
| AUPR064800A0 (en) | 2000-10-09 | 2000-11-02 | Usf Filtration And Separations Group Inc. | Improved membrane filtration system |
| AUPR094600A0 (en) | 2000-10-23 | 2000-11-16 | Usf Filtration And Separations Group Inc. | Fibre membrane arrangement |
| DE60213184T2 (en) | 2001-11-16 | 2007-06-28 | U.S. Filter Wastewater Group, Inc. | Method for cleaning membranes |
-
1999
- 1999-04-20 AU AUPP9850A patent/AUPP985099A0/en not_active Abandoned
-
2000
- 2000-04-20 CN CNB008064695A patent/CN1224449C/en not_active Expired - Lifetime
- 2000-04-20 EP EP00918589A patent/EP1189682B1/en not_active Expired - Lifetime
- 2000-04-20 ES ES00918589T patent/ES2354409T3/en not_active Expired - Lifetime
- 2000-04-20 WO PCT/AU2000/000352 patent/WO2000062908A1/en not_active Ceased
- 2000-04-20 NZ NZ514482A patent/NZ514482A/en not_active IP Right Cessation
- 2000-04-20 KR KR1020017013308A patent/KR100664619B1/en not_active Expired - Fee Related
- 2000-04-20 AT AT00918589T patent/ATE485883T1/en not_active IP Right Cessation
- 2000-04-20 DE DE60045155T patent/DE60045155D1/en not_active Expired - Lifetime
- 2000-04-20 JP JP2000612040A patent/JP4533539B2/en not_active Expired - Fee Related
-
2001
- 2001-10-18 US US10/045,186 patent/US20020148767A1/en not_active Abandoned
-
2003
- 2003-11-20 US US10/718,756 patent/US7264716B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JP4533539B2 (en) | 2010-09-01 |
| CN1347338A (en) | 2002-05-01 |
| EP1189682B1 (en) | 2010-10-27 |
| US20020148767A1 (en) | 2002-10-17 |
| NZ514482A (en) | 2003-04-29 |
| DE60045155D1 (en) | 2010-12-09 |
| WO2000062908A1 (en) | 2000-10-26 |
| EP1189682A4 (en) | 2003-01-02 |
| US7264716B2 (en) | 2007-09-04 |
| ATE485883T1 (en) | 2010-11-15 |
| ES2354409T3 (en) | 2011-03-14 |
| JP2002542013A (en) | 2002-12-10 |
| AUPP985099A0 (en) | 1999-05-13 |
| KR100664619B1 (en) | 2007-01-04 |
| US20040238431A1 (en) | 2004-12-02 |
| EP1189682A1 (en) | 2002-03-27 |
| KR20020026424A (en) | 2002-04-10 |
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